Process for removing hydrogen sulphide from gases



' may be omitted.

Patent d psept. 7, 19 26. in

UNITED- STAT S 1,598,985 PATENT OFFICE.

"IHEODOBUS 'ZPETRUS LUDOVICUS YETIT, OF VELSEN, NETHERLANDS.

PROCESS FOR REMOVING HYDROGEN SULPHIDE FROM GASES.

No Drawing. Application filed Karch 17,1923, Serial F0. 623,545, and in the Netherlands March- 16, 1922.

It is known that hydrogen sulphide can be removed from gases by washing the gas with a solution of alkali-metal carbonate or a suspension of alkaline earth carbonate and that thewashing liquid can be regenerated by conducting through it air which may or may not contain carbon dioxide. It is known that such presence 'of carbon dioxide facilitates the'regeneration. It is however not advantageous to use fiue gases for the regeneration, because they have many impurities andrequire an extensive purificationf a If flue gases were used, it would further benecessaryto heat the regenerated liquid in order to .convert into carbonate the bicarbonate which has been reduced, the car- ,bonate being required or the absorption When the air used for regeneration contains-less than 2 per cent of carbon dioxide, heating the liquid (at? expel carbon dioxide) et even then it is advantageous to convert-the bicarbonate into carbonate by warming as much as possible, because the pure carbonate absorbs sulphuretted' hydrogen much better than does carbonate, which is in equilibrium with a j not possible.

I used is that present carbonate in the regenerated washing liquid current of air at ordinary temperature, containing carbon dioxide.

' A process based 'onf-these lines has been followed. The H' S was absorbed b a solution containing 2-5 per cent of a,CO

' the regeneration was carried out by passing a large uantity of air through the solution; in t is process recovery of sulphur was By the present .invention regeneration of the alkali-metal carbonate solution by means of gases containing carbon dioxide becomes very advantageous when the carbon dioxide in. the form of biwhich has been freed from H S "According to liquid, which has been freed from H,S by a current of as containing carbon dioxide, is heated, wit or without passage of steam for inert gases through it, and the carbon dioxide thus liberated is used for expelling sulphuretted hydrogen from another supply liquid.

- The car on dioxide therefore is retained incirculation. In the regeneration process, when hydrogen sulphide is expelled, the car.- bon dioxide is absorbed and afterwards lib of washin the invention the washing because the gases that remove H 8 will also carry away-a part of the 00,. These losses however are fully compensated by the carfrom the unpurified gas together with the H S. This gas (town gas, coke oven gas, or the like) contains about 2 per cent of CO \Vith respect to known processes the indioxide and, after cooling, be-

bon dioxide which is absorbed by the liquid Y vention has in the first place the important advantage that a much smaller plant isrequired. In the second place no flue gasesare used and the difficult and expensive purification is thus eliminated. I

As compared with the regeneration process in which air with less than 2 per cent of CO is used without heating, it has the additional advantage that for absorbing H,S alkali-metal carbonate solutions are used which are wholly free from bicarbonate,so that a'much smaller absorptionplant is required. The heating of the bicarbonate so-t lution and the cooling of the carbonate solution before the absorption require little heat and little coolingwater, respectively, because heat exchange apparatus may be use to a large extent. The liquid coming from the absorption-apparatus may be used for coolin regenerated carbonate solution, and may thereby be preheated so that it loses H S more easily and for driving ofi H,S also only a small plant is required. Thesolution containing bicarbonate freed from H S, is therefore also somewhat preheated when it enters the apparatus in which the bicarbonate isdecomposed by heat, for in stance by means of auxiliary steam or air.

A furtheradvantage of the process is that the carbon dioxide content of the gas curquired for producing the gas current containing carbon dioxide.

A high percentage of carbon dioxide and a moderately raised temperature are favorable forsa high percentage of H 8 in the gas leaving the regenerating apparatus.

One may'choose the conditions most advantageous for each case.

One can control also in this manner to ya large extent the content of H 8 in, the gas current carrying the liberated .H S. The

-application of this H S is very much facilitated thereby, whether forthe production of sulphur or sulphuric acid 'or of some other product.

' As awashing liquid a solution of potash (for example, of25 per cent strength) is referred because the carbonate and bicarbonate of potassiumare more soluble than those of sodium so that a plant using potash maybe comparatively small in that it can use a strong solution.

What I claim is':

1, IA cyclic process of continuously removing hydrogen sulphide from gases, essenti'ally comprising the following steps in combination: washing the gas with an al kalimetal carbonate solution to absorb the hydro'gensulphide therefrom; passing a gas containi' "carbon dioxide through the washing 'solution to expel the absorbed hydrogen sulphidejfheating the solution thus obtained to regenerate "the alkali-metal carbonate solution decomposing the bicarbonate which was produced and to liberate excess carbon dioxide; passing through another supply of washing solution the liberated carbon ioxide in concentrated'condition; and then washing, with the regenerated alkalimetal carbonate solution, a fresh supply of the hydrogen-sulphide-containing gas.

A cyclic process of continuously removhydrogen sulphide from gases, esseniltiaily comprising the following steps in comb 'ation: washingithe gas with an alkalimetal carbonate solution to absorb the hydrogen sulphide therefrom; passing a gas containing carbon dioxide through the washing solution to expel the absorbed hydrogen sulphide; heating the solution thus obtained to regenerate the alkalimetal carbonate solution by decomposing the bicarbonate which was "producedand to liberate excess carbon dioxide; passing a current of' steam through the solution during the heating step; passing through another supply of washing solution the liberated carbon dioxide in concentrated condition; and then washing, with the regenerated alkali-metal carbonate solution, a fresh supply of the hydrogen-sulphide-containing gas.

3. A cyclic process of continuously removing hydrogen sulphide from gases, essentially comprising the following steps in com bination: washing the gas with a potassium carbonate solution to absorb the hydrogen sulphide therefrom; passing a gas containingcarbon dioxide through the potassium carbonate solution to expel the absorbed hydrogen sulphide; heating the solution thus obtained to regenerate the potassium carbonate solution by decomposing the bicarbonate which was produced and to liberate excess carbon dioxide; passing through another supply of used potassium carbonate washing solutionthe liberated carbon dioxide in concentrated condition; and'then washing, with the regenerated potassium carbonate solution thus treated, a fresh supply of the hydrogen-sulphide-containing gas.

ture.

THEODORUS PETRUS LUDOVICUS PETlT.

In testimony whereof I aflix my signa- 

